Method for purifying m-phenylenediamine
A technology of m-phenylenediamine and purification method, applied in the direction of amino compound purification/separation, organic chemistry, etc., can solve the problems of large reflux ratio, high equipment investment and operation energy consumption, and many theoretical plates, etc., to improve the utilization rate , Reduce separation energy consumption and equipment investment, the effect of scientific principle
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Embodiment 1
[0021] Embodiment 1: a kind of purification method of m-phenylenediamine, specifically comprises the following steps:
[0022] (1) The total content of diaminotoluene in m-phenylenediamine ashes is about 240ppm, of which about 80% is 2,4-diaminotoluene and about 20% is 2,6-diaminotoluene; The diamine ashes are continuously sent to the rectification tower with a theoretical plate number of 50; continuous rectification at 3kPa, the temperature at the top of the rectification tower is controlled at 162°C, the temperature at the bottom of the tower is 178°C, and m-phenylenediamine passes through the tower After the top condenser is cooled, the part is returned to the top of the tower through the reflux pipe as the reflux liquid, and the reflux ratio is controlled to be 5, and the liquid accounting for 60% of the total liquid quality is extracted through the m-phenylenediamine extraction pipe;
[0023] (2) Inject the mined m-phenylenediamine directly into the crystallizer, heat unt...
Embodiment 2
[0025] Embodiment 2: a kind of purification method of m-phenylenediamine, specifically comprises the following steps:
[0026] (1) The total content of diaminotoluene in m-phenylenediamine ashes is about 220ppm, of which about 80% is 2,4-diaminotoluene and about 20% is 2,6-diaminotoluene; The diamine ashes are continuously sent to the rectification tower with a theoretical plate number of 60; continuous rectification at 5kPa, the temperature at the top of the rectification tower is controlled at 180°C, the temperature at the bottom of the tower is 200°C, and m-phenylenediamine passes through the tower The cooled part of the top condenser is returned to the top of the tower through the reflux pipe as the reflux liquid, and the reflux ratio is controlled to be 8, and the liquid accounting for 45% of the total liquid mass is extracted through the extraction pipe;
[0027] (2) Inject the mined m-phenylenediamine directly into the crystallizer, heat until it is completely molten, c...
Embodiment 3
[0029] Embodiment 3: a kind of purification method of m-phenylenediamine, specifically comprises the following steps:
[0030] (1) The total content of diaminotoluene in m-phenylenediamine ashes is about 190ppm, of which about 80% is 2,4-diaminotoluene and about 20% is 2,6-diaminotoluene; The diamine ashes are continuously fed into the rectification tower with a theoretical plate number of 70; continuous rectification at 1kPa, the temperature at the top of the rectification tower is controlled at 150°C, the temperature at the bottom of the tower is 170°C, and m-phenylenediamine passes through the tower After the top condenser is cooled, the part is returned to the top of the tower through the reflux pipe as the reflux liquid, and the reflux ratio is controlled to be 10, and the liquid accounting for 30% of the total liquid quality is extracted through the m-phenylenediamine extraction pipe;
[0031] (2) Inject the mined m-phenylenediamine directly into the crystallizer, heat u...
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